Particle Containing a Graphite Based Nucleus Covered with at Least One Continuous or Discontinuous Layer, Processes for Preparing the Same and Their Uses

ABSTRACT

Process for preparing by crushing, a homogenous mixture of particles containing a conductive nucleus including at least one graphite and continuously or discontinuously coated with at least one material that is different from the one constituting the nucleus, the size of the particles of the nucleus being larger than the particles used for coating the nuclei by crushing the particles together. The mixtures of particles obtained show electrochemical and mechanical properties that enable them to be advantageously used in electrochemical batteries and in paints.

FIELD OF THE INVENTION

The present invention relates to new particles made of a graphite based conductive nucleus. The nucleus of these particles is at least partially coated with a second material. The outer surface of the nucleus is entirely or partly coated with the second material, which is of a kind and/or physical shape that is different from that of the nucleus.

The present invention also relates to processes allowing to prepare homogenous mixtures of coated particles of the invention, by crushing together particles intended to constitute the nucleus with particles of an interactive functional agent. The particles of the interactive functional agent are larger than the particles that constitute the nucleus of coated particles of the invention.

The present invention also relates to the uses of this new type of particles that possesses particularly interesting electrochemical and mechanical properties, for example as a material that constitutes electrodes for electrochemical generators and as an additive for paints.

STATE OF THE ART

Japanese Patent bearing number P2000-51121 describes a lithium based secondary battery made of an anode whose main component is carbon, and a cathode whose main component is a lithium containing transition metal oxide, and an electrolyte. The material of the cathode of which the cathode previously mentioned is made, contains a carbon modified surface that is coated with a Li₄Ti₅O₁₂ based spinelle structure. This material has an activity voltage higher than 1.2 volts, and at this voltage, it has limited passivation. This cathode material is obtained by mixing a lithium hydroxide and a titanium oxide with carbon in a colloidal solution. After drying and solidification, the mixture is treated at a temperature in the range between 400° and 1000° Celsius in a non oxidizing atmosphere.

U.S. Pat. No. 5,521,026 describes the preparation of polymer dispersions including large quantities of solid non conductive particles, by crushing the particles together in the presence of a non polar solvent. Spreading films intended for batteries and obtained from these polymer dispersions are more uniform and have lesser porosity.

The processes known to this day for the preparation of coated particles have for example the following disadvantages:

-   -   use of important quantities of toxic solvents;     -   bringing the process into operation is very long;     -   very high costs for example in the case of processes using         plasma deposition technologies;     -   lack of versatility with respect to the diversity of coated         particles that can be prepared by bringing a single process into         operation;     -   problems of agglomeration and very high particle size dispersion         with respect to particles that are prepared; and     -   a limitation with respect to the thickness of the coating that         can be deposited on the nucleus.

The coated particles known to this day have for example the disadvantage of showing an on uniform porosity that is detrimental to the power of batteries that include such materials.

A need therefore existed for a new process allowing the preparation of coated particles and which is free of at least one of the disadvantages of the processes of the prior art.

A need also existed for mixtures of new coated particles having at least one of the following properties:

-   -   homogenous distribution;     -   absence of small particles (fines);     -   good electrochemical capacity;     -   good security when incorporating them into batteries; and     -   good mechanical stability of the coating.

BRIEF DESCRIPTION OF THE FIGURES

FIG. 1: this figure schematically illustrates 3 distinct modes of operation of a process according to the present invention that allow a particle of graphite to be coated with different materials and by the mechano-melting method.

Method A schematically illustrates the coating of small size graphite (B) on a large size graphite (A) of prismatic shape.

Method B schematically illustrates the coating of the same graphite with ceramic.

Method C schematically illustrates the coating of the same graphite with metal particles.

FIG. 2: this figure is a schematic representation of the principle of coating graphite with different types of materials: graphite, ceramic and metal.

FIG. 3: this figure is a schematic representation of coating graphite with a multilayer of materials such as, a metal, a ceramic or a graphite as well as coating with layers consisting of mixtures of these materials.

FIGS. 4 and 5: these figures are pictures made with a scanning electron microscope (SEM) and showing the coating of a 20 micrometer graphite, with a graphite of a size that is respectively between 3 and 5 micrometers by using the mechano-melting method.

FIGS. 6A and 6B are SEM pictures of particles coated according to the invention as obtained in example A.

FIGS. 7A and 7B are SEM pictures of particles coated according to the invention as obtained in example C.

FIGS. 8A and 8B are SEM pictures of coated particles obtained in example F.

FIGS. 9A and 9B are SEM pictures of coated particles obtained in example G.

SUMMARY OF THE INVENTION

The present invention relates to a process which allows the production of particles consisting of a conductive nucleus including at least one graphite that is at least partly coated on its surface by crushing these particles together with smaller particles of an interactive functional agent having a predetermined particle size and which is of a kind and/or a shape that is different from that of the nucleus of the coated particle.

The particles thus obtained show particularly interesting electrochemical properties and are advantageously used for example as insulating or conductive material for the electrodes of an electrical generator.

GENERAL DEFINITION OF THE INVENTION

A first object of the present invention consists of a process allowing the preparation of a homogenous mixture of particles containing a graphite based conductive nucleus whose surface is at least partly coated, preferably at least 10%, more preferably at least 80% coated, with a coating based on a material that is different in composition or in physical shape from the material that constitutes the nucleus.

Advantageously, the homogenous mixture of coated particles obtained is characterized by a particle size distribution with one single peak, preferably obtained when a particle size determination is made with the Microtrac X100 apparatus of MICROTRAC and/or with a conversion rate ≧90%.

The process includes at least on step of crushing together the particles intended to constitute the nucleus of the coated particles, so-called nucleus-particles and whose average size is X, with particles of at least one interactive functional agent having an average size Y that is smaller than size X.

Advantageously, the nucleus-particles, as well as the coating-particles that are used show a small particle size dispersion that is preferably [-50%, +50%], i.e. the corresponding mixtures of particles X and particles Y do not contain particles whose size is not more than 50% larger nor smaller than 50% than size X, or size Y.

Within the framework of the present invention, the expression nucleus-particle including at least one graphite is concerned with the particles that constitute the nucleus of the coated particles of the invention and they are made of at least one graphite. These particles advantageously vary in particle size from 1 to 50 micrometers, and preferably the particle size is of the order of 20 micrometers.

Graphite that is present in the nucleus of the coated particles is indifferently a natural or synthetic graphite or a mixture of at least two thereof.

Within the framework of the present invention the expression interactive functional agent relates to an organic or inorganic material or a mixture thereof. This material ensures a double function that translates into a chemical transformation and a physical transformation of the elements that it contains. Thus, the surface of the nucleus is modified following coating with a layer of a selected material and formation of chemical bonds at the level of the surface of the nucleus. There is therefore a transformation of the interactive functional agent into a shape that is bound to the structure of the nucleus, and also a transformation inside the structure for example in the case of siloxanes that are converted into silica following heating and loss of oxygen.

Within the framework oft he present invention, the expression average size of the particles corresponds to the mid-height value at 50% (d50) of the distribution peak.

A graphite whose shape differs from that of the nucleus but falling into the same class of crystallinity, either high, i.e. for a d₀₀₂ lower or equal to 340, or low, i.e. with d₀₀₂ higher than 340, may also be used as interactive functional agent. By way of example, when the nucleus-particles are spherical or prismatic or a mixture thereof, then the coating-particles may for example be fibrous, C60 or C70.

Ceramics may also be used as interactive functional agent. Ceramics of the type TiO₂, Al₂O₃, ZrO₂, SiC, Si₃N₄ are preferably used. Those of the type TiO₂, and/or ZrO₂ and more particularly those having a particle size between 10 and 500 nanometers represent a particularly interesting variant.

Fluorine salts such as LiF or alkali-earth fluorides such as (LiF)CaF₂ may also be used.

Metals and alloys may also be used. Among the alloys, those of the metallic type and more particularly metallic alloys containing one of the elements of the group consisting of Si, Sn, Ag and Al are of particular interest.

The following may also be used as interactive functional agents: oxides, preferably oxides of the type MgO, Li₂CO₃ and SiO₂, and silicon oxides which have been shown to be particularly interesting.

The interactive functional agent may be selected from the group consisting of polymers that are in solid state at room temperature.

The following are preferred:

-   -   four branch polymers preferably having hybrid terminals, more         preferably those having acrylate (preferably methacrylate) and         alkoxy hybrid terminals (preferably alkoxy having 1 to 8 carbon         atoms, more preferably methoxy or ethoxy), or vinyl; at least         one branch (and preferably at least two branches) of said four         branch polymers being capable of giving rise to cross-linking;     -   polyoxypropylenes and polyoxyethylenes having a molecular weight         that advantageously varies from 150 to 20,000; and     -   polysiloxanes ([Si(R)-0]-) such as those of the type         poly(dimethyl)siloxane, poly(ethoxysiloxane),         poly(octamethyl)trisiloxane, preferably having a molecular         weight that varies from 150 to 10,000, more preferably         polyoxysiloxanes of the type         poly(dimethylsiloxane-co-methylphenylsiloxane) preferably having         a molecular weight of about 800; and     -   mixtures of at least two of the above. Four branch polymers are         defined more in detail in PCT Application WO/0363287         incorporated by reference.

Mixtures of interactive functional agents may also be used to carry out the process of the invention. Thus, by way of examples, the following two mixtures consisting of:

-   -   60% Poly(dimethylsiloxane) and 40% of TiO₂, and     -   54% Poly(dimethylsiloxane), 36% of TiO₂ and 10% Li₂CO₃.

Size X of the particles that constitute the nucleus and size Y of the particles used to constitute the coating of the nucleus are in accordance with the relationship Y/X<1. Preferably X is higher than Y by at least 150% and preferably by at least 200%. This characteristic plays an important role with respect to the uniformity of the mixtures of coated particles obtained.

According to an advantageous embodiment of the invention, the particles of size X and/or those of size Y that are used, have a physical shape of the cylindrical, prismatic and/or blade type.

The step of crushing the materials together is preferably carried out under an inert atmosphere so as to decrease the risks of evaporation of carbon because of the formation of CO₂.

The inert atmosphere that is used preferably consists of one or more inert gases. Preferably, there atmosphere used is one that consists of a gas selected from the group consisting of argon and nitrogen and mixtures of these gases, more preferably in the presence of substantially pure argon.

The crushing step of the process of the invention is advantageously carried out at a temperature between 20 and 1000° C., and preferably at a temperature between 25 and 800° C.

The crushing step advantageously lasts between 10 seconds and 4 hours. Preferably it lasts between 60 seconds and 3 hours.

The crushing step of the process of the invention may be carried out under dry condition or in the presence of water or an organic solvent. This solvent is advantageously selected from the group consisting of ketones, alkenes, alkanes, alcohols and mixtures of at least two of the above solvents.

Preferably, water, acetone, toluene, heptane, methanol or a mixture of at least two of the above solvents will be used.

Because of it non polluting character, water is the preferred solvent.

The residual solvent is preferably removed by extraction or evaporation at the end of the crushing step. Solvent removal is preferably carried out up to 90%.

The solvent is advantageously added before initiating the crushing step. For example, a mixture of coating-particles and solvent is prepared, and once the mixture is homogenized, nucleus-particles are added.

The quantity of solvent used represents between 1 and 10% of the weight of the coating-particles that are subject to crushing. Preferably, between 2 and 5% of solvent is used.

According to another particularly advantageous embodiment of the process of the invention, the sizes of the particles are selected so that the ratio Y/X varies between 0.17 and 0.6, preferably said ratio varies between 0.25 and 0.35.

The techniques used for crushing the particles together comprise the methods normally used in the technique under consideration. Thus, when crushing is carried out mechanically, the techniques used include for example, HEBM, jet air-milling, mechano-melting such as the one of Hosokawa type, hybridization, for example the one carried out by using a NHS-O system that is marketed by NAR—Japan, and/or a combination of these techniques.

According to an advantageous embodiment, crushing together of the particles is carried out by mechano-melting at a rotation speed of the device between 2000 and 3000 rotations/minute, preferably said rotation speed is between 2300 and 2700 rotations/minute. According to this embodiment, crushing advantageously lasts between 10 and 210 minutes, more preferably the duration is between 15 and 60 minutes.

According to another advantageous embodiment of the invention, the particles obtained from the mixture are ellipsoidal.

Advantageously, the tap density of the particles obtained by the process of the invention is at least twice higher than that of the initial mixture of the particles of size X and those of size Y that are used to start up said process. Preferably, the tap density of the final product is >0.9 g/cc, more preferably the tap density is ≧1 g/cc.

The process of the invention is advantageously implemented with particles of size X that have a specific surface area, measured with a scanning electronic microscope, that varies between 1 and 50 m²/g, still more preferably, the specific surface area is between 2 and 10 m²/g.

The specific surface area (BET) of the particles of size Y varies between 5 and 800 m²/g, preferably it varies between 10 and 500 m²/g,

When coating of the nucleus-particles is carried out with ceramic particles of an average size Yc, these particles are preferably selected so that the ratio Yc/X is lower than 1, and preferably so that the ratio is between 0.0008 and 0.007.

Particularly interesting results are obtained with electronically conductive ceramics. Such ceramics are preferably selected from the group consisting of nitrides, such as TiN and GaN.

When an electronically non-conductive ceramic is used, the latter is preferably selected from the group consisting of Al₂O₃ and BaTiO₃.

When an electronically semi-conductive ceramic is used, the latter is preferably selected from the group consisting of SiC and BaTiO₃.

According to a particularly interesting variant of implementation of the process of the invention, ceramic particles having an average particle size Yc such that 10 nm<Yc<1 μm, preferably such that 50 nm<Yc<150 nm, are used as interactive functional agent.

When the particles of average size Y are particles of an alloy (hereinafter called particles of size Ya), they advantageously at least in part consist of Al, Sn, Ag, Si or a mixture of at least two of the latter elements and the ratio Ya/X is such that 0.005>Ya/X>0.2, preferably said ratio verifies the relationship 0.007>Ya/X>0.0008.

A second object of the present invention consists of coated particles capable of being obtained by one of the processes that constitute the first object of the present invention.

These particles include a conductive nucleus, consisting of at least one graphite, that is continuously or discontinuously coated with at least one layer obtained from an interactive functional agent selected from the group consisting of a graphite of a kind and/or a shape that is different from the one constituting the nucleus but of the same crystallinity, ceramics, metals and alloys, for example metallic type alloys as well as mixtures of at least two of these agents.

Among these particles, the ones whose nucleus consists of a graphite with a purity higher than 95% are particularly interesting with respect to their electrochemical properties. To optimize electrochemical properties, when impurities are present in the nucleus, it is indeed important that they do not interfere with the electronic properties of said coated particle.

Thus, according to another particular embodiment of particles, there is achieved a coating that neutralizes the electronic interferences produced by the impurities that are present in the graphite nucleus. Such a protective coating consists of a material that is different from the impurity(ies) that is (are) present in the graphite nucleus and are capable of producing interfering reactions. By way of example of impurities that could be present in the graphite nucleus, those of the type Al₂O₃, SiO₂, iron oxide or sulfur may be mentioned.

The coated particles of the invention preferably are of a size between 7 and 100 micrometers, preferably the size of the nucleus is between 10 and 30 micrometers and coating of the nucleus is advantageously made of graphite and with an average thickness between 1 and 5 micrometers.

Another particularly interesting sub-family of particles of the invention consists of particles in which the coating of the nucleus consists of a ceramic having an average thickness between 50 and 150 nanometers.

Another particularly interesting sub-family of particles of the invention consists of particles, in which the nucleus is covered with two continuous and/or discontinuous consecutive layers, each layer preferably having respective thicknesses E₁ and E₂ comprised between 50 nanometers and 5 micrometers, by means of consecutive crushing steps. These double layer particles are prepared by using two consecutive crushing steps. The coated-particles obtained in the first crushing step now act as “nucleus” and the coating-particles used to provide the second coating are of a size that is substantially smaller than the size of the particles that are coated for a first time. The other operating conditions of the second crushing remain substantially similar.

Two consecutive layers may consist of a different material.

By way of example, a sub-family of multi-coat particles, according to the invention, consists of particles whose nucleus is covered with three layers, each of the 3 layers respectively having a thickness E₁, E₂, E₃ preferably between 50 nanometers and 5 micrometers and the thicknesses of the three layers being such that their sum is preferably smaller than 10 micrometers. In these three layer particles, each of the 3 layers may consist of a different material. It should be noted that the same approach is applicable for the preparation of these 3 coat particles as in the case of the 2 coat particles, except that it includes an additional step of crushing the double coat nucleus-particle together with coating-particles of a size substantially smaller than the size of the double coat particles. The other operating conditions for the third crushing remain substantially the same.

The multiple coating-particles thus prepared have particularly interesting electrochemical and mechanical properties, for example with respect to the electrochemical capacity and the operating safety of batteries including them, and this, thanks to the absence of important exothermic factors.

Particles comprising a graphite core that is covered in the amount of at least 80% of its external surface with said coating, have excellent electronic properties.

The mixtures of particles of the present invention have excellent electrical properties, for example an electronic conductivity that can vary between 10⁻²² and 10^(')Ohm⁻¹·cm⁻¹.

In the case of mixtures of particles in which the nucleus consists of graphite and the coating is of the metallic type, an electronic conductivity higher than 300 Ohm.⁻¹·cm⁻¹ can be measured.

In the case of a mixture of particles in which the coating consists of aluminum, the measured electronic conductivity is higher than 350 Ohm⁻¹·cm⁻¹ and in most cases even reaches higher values of about 377×103 Ohm⁻¹·cm⁻¹.

A third object of the present invention resides in the use of coated particles according to the second object of the invention, as insulating or conductive material for electrical generator electrodes.

According to an advantageous embodiment, particles coated with CeO₂, Li₃PO₄, graphite-Ag, Li₂CO₃ and/or MgO-graphite, Li₂CO₃—Li are used in fuel cells. In this application, the particles are used for the purpose of storing energy.

A fourth object of the present invention resides in the use of the coated particles of the invention, for example made of polymers-graphites, in coatings, preferably in paints. In this application, the coated particles are used as additives for reinforcing for example the mechanical properties of the paint film formed.

Definition of Preferred Embodiment of the Invention

Crushing fibrous graphite together with spherical graphite is obtained by mixing a graphite of a 20 μm particle size with another graphite having a particle size that varies from 2 to 7 μm. This crushing is obtained by dry mixing or mixing with a solvent while using a high energy ball mill “HEBM” from Spex, by mechano-melting of the Hosokawa type or by “hybridization” of the Nara type. The natural or artificial particle of graphite that originally was prismatic, acquires a new ellipsoidal shape.

Li₂Ti₂O₃ is mixed with a graphite of particle size 20 μm. This mixture is obtained by HEBM in a dry or liquid medium or by mechano-melting. The tap density of the mixture and the final particle avec converted into ellipsoidal shape. The mixture of three elements crushed together is carried out from natural 20 μm graphite with a Sn type metallic powder and a ceramic of the type Li₂Ti₂O₃. The graphite-metal mixture is crushed with HEBM (dry or in a solvent) or by mechano-melting or by hybridization, and the particle becomes ellipsoidal.

It is thus observed that there is an increase of the tap density of the electrode (generally expressed in grams per cm³), of the kinetics and that there is insertion of lithium in the graphite.

EXAMPLES

The following examples are given purely by way of illustration and should not be interpreted as constituting any limitation of the invention.

Method A: Crushing Graphite Together with Graphite

The core particle of natural graphite has an average size of 20 μm and is prismatic. This graphite is mixed with a spherical graphite of a particle size between 2 and 7 μm. The small size particles of graphite are used for coating the 20 μm particles of graphite. Crushing is obtained by HEBM or by mechano-melting (of the Hosokawa type).

Method B: Crushing Graphite Together with Ceramic.

Crushing is carried out par mixing a 20 μm natural prismatic graphite together with 10% of Li₂Ti₂O₇ of a particle size smaller than 1 μm (sub-micron). The natural graphite is coated with the particles of ceramic, and becomes ellipsoidal. This crushing is obtained by HEBM or by mechano-melting (of the Hosokawa type).

The electronic properties of the ceramic do not affect the transformation of the prismatic particle into an ellipsoidal crushed product. The possibility of inserting lithium into the ceramic, that surrounds the graphite, is superposed over the possibility of inserting lithium into the graphite.

Method C: Crushing Graphite Together with a Metal

This method utilizes natural prismatic 20 μm graphite that is mixed together with 20% of a nanometric tin (Sn) powder. This mixture is crushed by mechano-melting of the Hosokawa type. In this way, the prismatic shape of graphite is converted into an ellipsoidal shape. Insertion of lithium into the Sn metal leads to an alloy (LixSny) having a higher possibility as compared to that of inserting lithium into graphite. Formation of the metallic alloy gives rise to a supplement of mass (mAh/g) and volume (mAh/l) capacity at the electrode. There is thus an increase of density of mass (Wh/kg) and volume energy (Wh/l) of the battery.

EXAMPLE

A Brazilian natural graphite with a particle size of 350 μm (starting material) is reduced to 20 μm by Jet-milling (graphite-A). Graphite B has a particle size that varies from 2 to 10 μm, and is obtained by jet milling the starting graphite. The tap density of graphite A and graphite B is about 0.35 g/cc.

A mixture of 80% graphite A and 20% of graphite B is introduced into a mechano-melting device of the Hosakawa type model AMS-Lab during 30 minutes. The product obtained has a tap density of 0.75 g/cc and an ellipsoidal shape.

It therefore seems that, in the case of insertion into a natural or artificial graphite, the kinetics of lithium is limited by the prismatic shape of the particles of these materials (1). In these materials, the portion of the basal planes f_(b) is predominant as compared to the edge portion f_(e). Their tap density is low (0.2-0.3 g/cc) because of the prismatic shape of their particles. Thus, the kinetics and diffusion of lithium in graphite was increased by transformation of the prismatic shape into ellipsoidal. This ellipsoidal shape reduces the portion f_(b) which appears to represent the limiting barrier for the insertion of lithium into graphite.

This advantageous ellipsoidal shape has thus been obtained by way of illustration by the three methods hereinabove described, and moreover, with a minimum amount of starting materials.

Example A—Li₂CO₃ Based Coating

A mixture consisting of 500 grams of particles of a graphite type is used as first starting component.

The particles of the mixture have an average size of 20 microns and are prismatic. They are treated with a mechano-melting, device such as those marketed by Hosokawa in Japan, during 15 minutes and at a temperature of 25 degrees Celsius.

Under the effect of this treatment, the surface of the particles of graphite is modified and results in a spherical shape. The mixture thus obtained is designated graphite SNG20.

45 grams of the SNG20 mixture are mixed with 5 grams of Li₂CO₃ (μ) and the mixture is treated during 25 seconds with a hybridizer sold by NARA of Japan.

The particles of graphite thus obtained contain a coating including 10% of lithium carbonate (Li₂CO₃) and 90% graphite.

Pictures of these particles are shown in FIGS. 6A and 6B.

Example B (Coating of Li₂CO₃+LiF)

45 grams of the SNG20 mixture are mixed with 2.5 grams of Li₂CO₃ and with 2.5 grams of LiF. The thus prepared mixture is treated during 25 seconds with a hybridizer (NARA, Japan).

The particles of graphite obtained are characterized by a hybrid coating comprising Li₂CO₃ and LiF.

Example C (Coating of Si): HEBM+MECHANO+Hybridizer

A macroscopic powder consisting of Si particles 2 microns is crushed in a Spex HEBM (High Energy Ball Milling) during 2 hours which gives a nano powder of Si.

A mixture consisting of 45 grams of spherical particles of graphite SNG20 is mixed with 5 grams of Si (μ) and treated during 25 seconds with a hybridizer (NARA, Japan).

The particles of graphite thus obtained contain a coating based on particles of nano-Si, whose size is smaller than 500 nanometers.

The particles obtained are visible on the pictures of FIGS. 7A and 7B.

Example D (Coating of Si): HEBM+MECHANO

A 2 micron macroscopic powder of Si is crushed in a Spex HEBM (High Energy Ball Milling) during 2 hours to give Nano Si.

A mixture of 45 grams of particles of graphite SNG20 is mixed with 5 grams of particles of nano Si, during 15 minutes, by mechano-melting (Hosokawa, Japan).

The particles of graphite thus obtained include a coating based on particles of nano-Si, smaller than 500 nanometers.

Example E (Coating of Si): HEBM+INOMISER+HYBRIDIZER

A macroscopic powder of silicon (Si) particles, average size 2 microns, is crushed in a Spex HEBM (High Energy Ball Milling) during 2 hours and the result is a mixture of particles of silicon.

45 grams of a mixture of particles of graphite SNG20 obtained in example A are mixed with 5 grams of particles of silicon of an average size of 500 nanometers, during 25 seconds, by means of a hybridizer (NARA, Japan).

Example F (Synthesis as a Function of Silicon Oil)

A mixture of particles of graphite SNG20 obtained in example A and silicon oil in the weight ratio of (10:20) is produced with HEBM.

The mixture is heated during 4 hours under controlled atmosphere (Argon).

Pictures of the coated particles thus obtained are identified in FIGS. 8A and 8B.

Example G (Synthesis of Particles Coated as a Function of an Alloy of Siloxane Polymer and ERM)

A mixture consisting of particles of graphite of the type SNG20 and a hybrid 4 branch polymer (PEO-PPO) Siloxane-ERM (1:1), of DKS, in the weight ratio (80:20) is prepared by HEBM.

The mixture is heated during 4 hours under controlled atmosphere (Argon), at a temperature of 500 degrees Celsius.

The particles of graphite thus prepared have 10 to 30% of their surface covered with silicon and amorphous carbon. They are visible on the pictures identified FIGS. 9A and 9B.

Amorphous carbon results from a pyrolysis of the polymer of type ERM. This carbon ensures a double role, the first one being to provide electronic conduction bridges between graphite and the alloy of silicon, once lithium has been inserted into silicon.

In view of the porosity of the carbon thus formed at the surface of the particles, the second function of carbon is to absorb the volume expansion of the alloy.

On the other hand, an improvement of the homogeneity of the mixtures of particles obtained by the process of the invention has been established in the following manner.

There is provided a known mixture of two types of particles, namely particles of type Si or Li₂CO₃ of particle size 500 nm (d50) D10, 300 nm and D90, 1 micron, with particles of graphite of particle size 20 microns (d50) D10, 10 microns and D90 28 microns.

The mixture thus obtained in known manner, by simple mixing, has shown during a particle size analysis carried out with the apparatus Micro Trac X100 of Horiba, two relative peaks at concentrations of 0.5 micron and 20 microns.

On the other hand, when carrying out an intimate crushing by mechano-melting or with a Hybridizer according to the process of the invention, the particle size analysis shows a single peak at 20 microns.

These results demonstrate the fact that the particles of graphite are completely coated with particles of the Type Si or Li₂CO₃. On the other hand, these experimental results reveal an excellent force of contact between the small particles and the graphite nucleus.

Although the present invention has been described with specific embodiments, it is understood that many variations and modifications may be grafted to said embodiments, and the present invention aims at covering such modifications, uses or adaptations of the present invention following in general, the principles of the invention and including any variation of the present description which will become known or conventional in the field of activity in which the present invention in found, and which may be applied to the essential elements mentioned above, in accordance with the scope of the following claims. 

1. Process for preparing a homogenous mixture of coated particles containing a graphite based conductive nucleus and at least one partial or complete coating of the surface of said nucleus, the coating being based on an interactive functional agent consisting of a material that differs in composition and/or in physical shape from the material that constitute the nucleus of the coated particles, said process including at least one step of crushing particles of the graphite nucleus together with particles of the interactive functional agent, the particles of graphite having an average size Y and those of the interactive functional agent having an average size X such that the ratio Y/X is smaller than
 1. 2. Process according to claim 1, in which the interactive functional agent is selected from the group consisting of: graphite having a shape that differs from that of the graphite(s) that constitute(s) the nucleus but belonging to the same class of crystallinity; ceramics (preferably ceramics of the type TiO₂.Al₂O₃, ZrO₂, SiC, Si₃N₄, still more preferably those of the type TiO₂, and/or ZrO₂); fluoride salts such as LiF or alkaline-earth fluorides such as (LiF)CaF₂; metals and alloys (preferably alloys of the metallic type, still more preferably the metallic alloys containing one of the elements of the group consisting of Si, Sn, Ag, and Al); oxides, preferably oxides of the type MgO, Li₂CO₃ and SiO₂; polymers that are solid at room temperature such as: four branch polymers preferably having hybrid terminals, still more preferably those having hybrid acrylate terminals (preferably methacrylate) and alkoxy (preferably alkoxy with 1 to 8 carbon atoms, still more preferably methoxy or ethoxy), or vinyl; one branch at least (and preferably at least two branches) of said four branch polymer being capable of giving rise to cross-linking, polyoxypropylenes and polyoxyethylenes with an average molecular weight that advantageously varies from 150 to 20,000, polysiloxanes ([Si(R)—O]—) such as those of the type poly(dimethyl)siloxane, poly(ethoxysiloxane), poly(octamethyl)trisoloxane, preferably having a molecular weight that varies from 150 to 10,000, still more preferably polyoxysiloxanes of the type Poly(dimethylsiloxane-co-methylphenylsiloxane) preferably having a molecular weight of about 800; and mixtures of at least two of the above.
 3. Process according to claim 1, in which the size of the particles that are subject to crushing is selected so that X is at least 150%, and preferably at least 200% higher than Y.
 4. Process according to claim 1, in which at least 10%, preferably at least 80%, of the surface of the nuclei is covered with a coating.
 5. Process according to claim 1, in which the homogenous mixture of coated particles obtained is characterized by a size distribution having a single peak, preferably when the particle size is measured with the Microtrac X100 apparatus of MICROTRAC and/or by means of a conversion rate ≧90%.
 6. Process according to claim 1, in which the crushing step is carried out under inert atmosphere, preferably consisting of a gas selected from the group consisting of argon and nitrogen and mixtures thereof, still more preferably in the presence of argon.
 7. Process according to claim 1, in which the crushing step is carried out at a temperature between 20 and 1000° C., preferably at a temperature between 25 and 800° Celsius.
 8. Process according to claim 1, in which the crushing step is carried out for a period during 10 seconds to 4 hours, preferably during 60 seconds to 3 hours.
 9. Process according to claim 1, in which the crushing step is carried out in the presence of a solvent preferably selected from the group consisting of water, organic solvents, inorganic solvents, and mixtures of at least two thereof, preferably the solvent is selected from the group consisting of water, ketones, alkenes, alkanes and alcohols, still more preferably the solvent is selected from the group consisting of water, acetone, toluene, heptane, methanol and mixtures thereof with water.
 10. Process according to claim 1, in which the solvent used is water.
 11. Process according to claim 9, in which the quantity of solvent used represents from 1 to 10% and preferably from 2 to 5% by weight of the total weight of the coating-particles that are present in the mixture of particles subject to crushing.
 12. Process according to claim 1, in which the particles of size X and/or those of size Y are cylindrical, prismatic and/or in the form of blades.
 13. Process according to claim 1, in which the X/Y ratio varies between 0.17 and 0.6, preferably said ratio varies between 0.25 and 0.35.
 14. Process according to claim 1, in which the crushing is carried out mechanically, preferably by HEBM, by jet air-milling, by mechano-melting of the Hosokawa type, by hybridization (preferably by using a NHS-O system marketed by NAR- Japan) and/or by using a combination of these techniques.
 15. Process according to claim 14, carried out by mechano-melting at a rotation speed of the installation between 2000 and 3000 rotations/minute, preferably said rotation speed is between 2300 and 2700 rotations/minute.
 16. Process according to claim 15, implemented for a period between 10 and 210 minutes, still more preferably for a period between 15 and 60 minutes.
 17. Process according to claim 1, in which the particles of the mixture obtained are ellipsoidal.
 18. Process according to claim 1, in which the tap density of the mixture of particles obtained is at least twice higher that that of the particles of size X that are used when starting said process.
 19. Process according to claim 18, in which the tap density of the final product is >0.9 g/cc, preferably the tap density is ≧1 g/cc.
 20. Process according to claim 1, in which the specific surface area (BET) of the particles of size X varies between 1 and 50 m²/g, preferably the specific surface area is between 2 and 10 m²/g.
 21. Process according to claim 1, in which the specific surface area (BET) of graphite Y varies between 5 and 800 m²/g, preferably said specific surface area varies between 10 and 500 m²/g.
 22. Process according to claim 1, in which the particles of average size Y are ceramic particles hereinafter designated particles of size Yc.
 23. Process according to claim 22, in which the Yc/X is lower than 1, preferably said ratio is between 0.0008 and 0.007.
 24. Process according to claim 22, in which the ceramic is electronically conductive, and is preferably selected from the group consisting of nitrides, such as TiN and GaN.
 25. Process according to claim 21, in which the ceramic is electronically non-conductive and is preferably selected from the group consisting of Al₂O₃ and BaTiO₃.
 26. Process according to claim 21, in which the ceramic is electronically semi-conductive and is preferably selected from the group consisting of SiC and BaTiO₃.
 27. Process according to claim 21, in which the particles of ceramic have an average size Yc such that 10 nm<Yc<1 μm, preferably such that 50 nm<Yc<150 nm.
 28. Process according to claim 1, in which the particles of average size Y are particles of an alloy (hereinafter designated particles of size Ya) consisting at least in part of Al, Sn, Ag, Si or a mixture of at least two thereof.
 29. Process according to claim 28, in which ratio Ya/X is such that 0.005>Ya/X>0.2, preferably said ratio verifies the relationship 0.007>Ya/X>0.0008.
 30. Process for preparing a homogenous mixture of coated particles according to any one of claim 1, said coated particles including a graphite based conductive nucleus and at least two partial or complete coatings of said nucleus, the coating particles obtained in the first crushing step being subject to a second crushing in the presence of an interactive functional agent that is identical or different from the first interactive functional agent used in the first crushing step, the average size of the particles of the second interactive functional agent being smaller than the size of the coated particles obtained in the first crushing step.
 31. Process according to claim 30, in which the coated particles that are prepared include a graphite based conductive nucleus and at least three partial or complete coatings of said nucleus, the coated particles obtained in the second step of crushing being subject to a third crushing in the presence of an interactive functional agent that is identical to or different from the interactive functional agents used in the first two crushing steps, the average size of the particles of the third interactive functional agent being smaller than that of the coated particles obtained in the second crushing step.
 32. Coated particle capable of being obtained by one of the processes according to claim
 1. 33. Particle containing a nucleus that at least partially consists of graphite, said particle being continuously or discontinuously coated with at least one layer of a material obtained from an interactive functional agent selected from the group consisting of graphite, ceramics, metals and alloys (such as alloys of metallic type) as well as mixtures of at least two thereof.
 34. Particle according to claim 32, consisting of a graphite nucleus with a purity higher than 95%.
 35. Particle according to claim 34, in which the impurities that are present in the nucleus do not interfere with the electronic properties of said particle.
 36. Particle according to claim 35, in which the coating of the nucleus neutralizes electronic interferences generated by the impurities that are present in the graphite nucleus.
 37. Particle according to claim 32, in which the size of the nucleus is between 7 and 100 micrometers, preferably the size of the nucleus is between 10 and 30 micrometers.
 38. Particle according to claim 32, in which the coating of the nucleus is made of graphite and has an average thickness between 1 and 5 micrometers.
 39. Process according to claim 32, in which the coating of the nucleus is made of a ceramic and has an average thickness between 50 and 150 nanometers.
 40. Particle according to claim 32, in which the nucleus is covered with two consecutive continuous and/or discontinuous layers, each of the layers preferably having respective thicknesses E₁ and E₂ comprised between 50 nanometers and 5 micrometers.
 41. Particle according to claim 40, in which each of the 2 layers consists of a different material.
 42. Particle according to claim 32, in which the nucleus is covered with three layers, each of the 3 layers respectively having a thickness E₁, E₂, E₃ preferably comprised between 50 nanometers and 5 micrometers and the thicknesses of the three layers being such that their sum is preferably lower than 10 micrometers.
 43. Particle according to claim 42, in which each of the 3 layers consists of a different material.
 44. Particle according to claim 32, consisting of a graphite core wherein at least 80% of its external surface is covered with said coating.
 45. Mixture of particles as obtained by implementation of one of the processes defined in claim 1 and having at least one of the following properties: an electronic conductivity between 10⁻²² and 10³ Ohm⁻¹·cm⁻¹; and a particle size distribution preferably restricted between −50%, +50%.
 46. Mixture of particles according to claim 45, in which the nucleus consists of graphite, the coating is of metallic type and the electronic conductivity is higher than 300 Ohm⁻¹·cm⁻¹.
 47. Mixture of particles according to claim 46, in which the coating consists of aluminum and the electronic conductivity is higher than 350 Ohm⁻¹·cm⁻¹, preferably higher than about 377×103 Ohm⁻¹·cm⁻¹.
 48. Use of the particles according to claim 47 as insulating material or conductor for an electrode of an electrical generator.
 49. Use of particles according to claim 45, coated with CeO₂, Li₃PO₄, graphite-Ag and/or MgO-graphite in fuel cells.
 50. Use of particles according to claim 48, coated with polymers-graphite, in coatings, preferably paints.
 51. Particle according to claim 33, in which the size of the nucleus is between 7 and 100 micrometers, preferably the size of the nucleus is between 10 and 30 micrometers.
 52. Particle according to claim 33, in which the coating of the nucleus is made of graphite and has an average thickness between 1 and 5 micrometers.
 53. Process according to claim 33, in which the coating of the nucleus is made of a ceramic and has an average thickness between 50 and 150 nanometers.
 54. Particle according to claim 33, in which the nucleus is covered with two consecutive continuous and/or discontinuous layers, each of the layers preferably having respective thicknesses E₁ and E₂ comprised between 50 nanometers and 5 micrometers.
 55. Particle according to claim 54, in which each of the 2 layers consists of a different material.
 56. Particle according to claim 33, in which the nucleus is covered with three layers, each of the 3 layers respectively having a thickness E₁, E₂, E₃ preferably comprised between 50 nanometers and 5 micrometers and the thicknesses of the three layers being such that their sum is preferably lower than 10 micrometers.
 57. Particle according to claim 56, in which each of the 3 layers consists of a different material.
 58. Particle according to claim 33, consisting of a graphite core wherein at least 80% of its external surface is covered with said coating.
 59. Mixture of particles as defined in claim 33 and having at least one of the following properties: an electronic conductivity between 10⁻²² and 10³ Ohm⁻¹·cm⁻¹; and a particle size distribution preferably restricted between [−50%, +50%].
 60. Mixture of particles according to claim 59, in which the nucleus consists of graphite, the coating is of metallic type and the electronic conductivity is higher than 300 Ohm⁻¹·cm⁻¹.
 61. Mixture of particles according to claim 60, in which the coating consists of aluminum and the electronic conductivity is higher than 350 Ohm⁻¹·cm⁻¹, preferably higher than about 377×103 Ohm⁻¹·cm⁻¹.
 62. Particle according to claim 33, consisting of a graphite nucleus with a purity higher than 95%.
 63. Particle according to claim 48, in which the impurities that are present in the nucleus do not interfere with the electronic properties of said particle.
 64. Particle according to claim 49, in which the coating of the nucleus neutralizes electronic interferences generated by the impurities that are present in the graphite nucleus.
 65. Use of the particles according to claim 61 as insulating material or conductor for an electrode of an electrical generator.
 66. Use of particles according to claim 59, coated with CeO₂, Li₃PO₄, graphite-Ag and/or MgO-graphite in fuel cells.
 67. Use of particles according to claim 65, coated with polymers-graphite, in coatings, preferably paints. 